US2081168A - Method of preventing scale depositions and removing such deposits from metallic surfaces - Google Patents
Method of preventing scale depositions and removing such deposits from metallic surfaces Download PDFInfo
- Publication number
- US2081168A US2081168A US608863A US60886332A US2081168A US 2081168 A US2081168 A US 2081168A US 608863 A US608863 A US 608863A US 60886332 A US60886332 A US 60886332A US 2081168 A US2081168 A US 2081168A
- Authority
- US
- United States
- Prior art keywords
- deposits
- sludge
- metallic surfaces
- water
- preventing scale
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
Definitions
- the invention comprises an aqueous solution vof a composition including ammonia and purified sludge recovered from the treatment of petroleum oils with concentrated sulphuric acid. There is formed by the treatment of mineral oils such as lubricating oils, with large quantities of concentrated sulphuric acid, an acid or group of acids and other-materials which separate out in an acid sludge layer. 5 The sludge layer is purified by removing the -oil and sulphuric acid as follows: The sludge resulting from the concentrated sulphuric acid treatment of mineral oils after separating from the oil layer is first washed with a medium heavy petroleum distillate. This removes a considerable portion of the oil.
- the remaining sludge is diluted with water sufficient to form two layers after agitation with steam.
- the mixture after being thoroughly agitated with steamis allowed to settle and stratify, and the water layer containing the major portion of the sulphuric acid present in the sludge is removed.
- the sludge layer is extracted withnaphtha for removal of the remaining oil.
- the separated sludge layer containing the sludge acids and other materials is now suitable for use in our compositions.
- the following composition is given for' illustration.
- the quantity of ammonia added is sufliient to neutralize the sludge acids present and a 40 slight excess is not detrimental.
- ammonia-neutralized sludge is introduced either into the cooling tower reservoir ,or into the hot well, daily or weekly. ln varying amounts depending on the water to be treated. If too much ammonia-neutralized sludge is added, an excessive foaming results and this foaming is a measure of the amount required fortreating.
- a preliminary test of the water may be used as a'guide to the amount of ammonianeutralized sludge required to treat adeflnite quantity of water. A measured quantity ofwater isjtaken and measured amounts of ammonianeutralized sludge are slowly added while constantly stirring the water until foaming of the mixture results. The largest proportion of ammonia-neutralizedlsludge that may be added without foaming -is.used.
- Oilstock tanks and pipe lines, natural gasoline plant equipment, etc.. are also. protected from the corrosive action of hydrogen sulphide and other deleterious compounds by coating both inside and outside'with this composition; It is insoluble in oil and is not dissolved from-the walls of the containers and-pipes formingan.efl'ectiveprotection for the surface. v
- the method of preventing scale depositions and removing such deposits from metallic surfaces which comprises subjecting the surface to the action of an aqueous'solution of ammonium
- the composition likewise prevents scale'forma-' salt of water soluble sulfonic acid resulting from the treatment of petroleum with concentrated sulfuric acid, said aqueous solution being substantially free from oil and from acids and containing a slight excess of ammonia, the sulfonic acid salt. also being in the largest proportion permissible without foaming.
Description
Patented May 25, 1937 UNITED STATES PATENT OFFICE METHOD OF PREVENTING SCALE DEPOSI- TIONS AND REMOVING SUCH DEPOSITS FROM METALLIC SURFACES Boris S..de Mei-ing, Houston, Tex., assignor to Standard Oil Development Company, a cor-' poration of Delaware NoDrawing. Application May 2, 1932, Serial No. 608,863
. 4 Claims. ((187 -27) In its preferred form the invention comprises an aqueous solution vof a composition including ammonia and purified sludge recovered from the treatment of petroleum oils with concentrated sulphuric acid. There is formed by the treatment of mineral oils such as lubricating oils, with large quantities of concentrated sulphuric acid, an acid or group of acids and other-materials which separate out in an acid sludge layer. 5 The sludge layer is purified by removing the -oil and sulphuric acid as follows: The sludge resulting from the concentrated sulphuric acid treatment of mineral oils after separating from the oil layer is first washed with a medium heavy petroleum distillate. This removes a considerable portion of the oil.
The remaining sludge is diluted with water sufficient to form two layers after agitation with steam. The mixture after being thoroughly agitated with steamis allowed to settle and stratify, and the water layer containing the major portion of the sulphuric acid present in the sludge is removed. The sludge layer is extracted withnaphtha for removal of the remaining oil.
The separated sludge layer containing the sludge acids and other materials is now suitable for use in our compositions. The following composition is given for' illustration.
A quantity of the sludge layer, separated as described, containing about 20 to 35% of sludge acids, is dissolved in an equal quantity of water and ammonia is added slowly with constant stirring. The quantity of ammonia added is sufliient to neutralize the sludge acids present and a 40 slight excess is not detrimental.
In treating water used in the water jackets of engines, ammonia-neutralized sludge is introduced either into the cooling tower reservoir ,or into the hot well, daily or weekly. ln varying amounts depending on the water to be treated. If too much ammonia-neutralized sludge is added, an excessive foaming results and this foaming is a measure of the amount required fortreating. A preliminary test of the water may be used as a'guide to the amount of ammonianeutralized sludge required to treat adeflnite quantity of water. A measured quantity ofwater isjtaken and measured amounts of ammonianeutralized sludge are slowly added while constantly stirring the water until foaming of the mixture results. The largest proportion of ammonia-neutralizedlsludge that may be added without foaming -is.used.
Oilstock tanks and pipe lines, natural gasoline plant equipment, etc.. are also. protected from the corrosive action of hydrogen sulphide and other deleterious compounds by coating both inside and outside'with this composition; It is insoluble in oil and is not dissolved from-the walls of the containers and-pipes formingan.efl'ectiveprotection for the surface. v
and removing such deposits from metallic surfaces which comprises subjecting the surface to the action of an aqueous solution of an ammo,- nium salt of a water soluble sulfonic acid resulting from the treatment of petroleum with concentrated sulfuric acid, said aqueous solution being substantially free from oil'and from free acids and containing a sufficient amount of said salt to prevent scale deposition on and to remove such deposits from metallic surfaces.
2. The method of preventing scale depositions and removing such deposits from metallic surfaces, which comprises subjecting the surface to the action of an aqueous'solution of ammonium The composition likewise prevents scale'forma-' salt of water soluble sulfonic acid resulting from the treatment of petroleum with concentrated sulfuric acid, said aqueous solution being substantially free from oil and from acids and containing a slight excess of ammonia, the sulfonic acid salt. also being in the largest proportion permissible without foaming.
3. The method of-pi'eventing scale formation and removing scale deposits from the water jacket of an engine which comprises adding to the water circulated through said jacket an ammonium salt of a-water soluble sulfonic acid resulting from the treatment of petroleum with concentrated sulfuric acid, the resulting solution being substantially free from oil'and from free acids and in the largest proportion permissible without foaming. I
4. Process according to' claim 3 in which the solution contains from about 10 to Ti of the ammonium salt. Y
' BORIS S. on MERING;
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US608863A US2081168A (en) | 1932-05-02 | 1932-05-02 | Method of preventing scale depositions and removing such deposits from metallic surfaces |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US608863A US2081168A (en) | 1932-05-02 | 1932-05-02 | Method of preventing scale depositions and removing such deposits from metallic surfaces |
Publications (1)
Publication Number | Publication Date |
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US2081168A true US2081168A (en) | 1937-05-25 |
Family
ID=24438356
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US608863A Expired - Lifetime US2081168A (en) | 1932-05-02 | 1932-05-02 | Method of preventing scale depositions and removing such deposits from metallic surfaces |
Country Status (1)
Country | Link |
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US (1) | US2081168A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2577626A (en) * | 1947-06-20 | 1951-12-04 | Standard Oil Dev Co | Preventing corrosion of metals |
US2727788A (en) * | 1951-07-03 | 1955-12-20 | Diamond Alkali Co | Electrolytic cell cleaning apparatus |
US3132052A (en) * | 1962-08-20 | 1964-05-05 | Dow Chemical Co | Method of removal of organic fouling deposits employing nitrosylsulfuric acid composition |
US5965094A (en) * | 1995-06-05 | 1999-10-12 | C.I.R.S. S.P.A. | Polymerization process with anti-scaling agents |
-
1932
- 1932-05-02 US US608863A patent/US2081168A/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2577626A (en) * | 1947-06-20 | 1951-12-04 | Standard Oil Dev Co | Preventing corrosion of metals |
US2727788A (en) * | 1951-07-03 | 1955-12-20 | Diamond Alkali Co | Electrolytic cell cleaning apparatus |
US3132052A (en) * | 1962-08-20 | 1964-05-05 | Dow Chemical Co | Method of removal of organic fouling deposits employing nitrosylsulfuric acid composition |
US5965094A (en) * | 1995-06-05 | 1999-10-12 | C.I.R.S. S.P.A. | Polymerization process with anti-scaling agents |
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